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We have detected formate synthesis by Clostridium thermocellum 27405 cultured in both cellobiose and alpha-cellulose. While formate synthesis has been reported for one strain of C. thermocellum (strain I-1-B), numerous studies of C. thermocellum 27405 fermentation, conducted under different growth conditions, failed to detect the presence of formate. Thus, the status of formate synthesis as a fermentation end product by C. thermocellum has been uncertain. Formate synthesis competes with the synthesis of hydrogen (H2) as a fermentation end product, and thus would negatively impact H2 yields in processes designed to generate H2 from biomass. Understanding the mechanism of formate synthesis is the first step in devising means of mitigating its production. Transcription of putative pfl, fnr, and adhE genes, encoding pyruvate formate-lyase (PFL), PFL-activating enzyme (PFL-AE), and alcohol dehydrogenase E (ADH-E) enzymes, respectively, were detected by reverse transcriptase polymerase chain reactions using total RNA extracted from stationary phase C. thermocellum cultured on cellobiose. The PCR products observed correspond to the expected amplicon sizes. Nucleotide sequence analysis of the cloned PCR products followed by BLAST analyses confirmed their identity. Formate production was detected throughout growth, and PFL enzyme activity was detected in late log and stationary phase (OD600 = 0.7 and 0.9, respectively) in extracts of C. thermocellum cultured on cellobiose. BLAST analyses revealed that C. thermocellum PFL and PFL-AE have greater amino acid sequence identity with equivalent enzymes from Bacillus and Thermocynechococcus species than with other Clostridium species, but C. thermocellum ADH-E has greater amino acid sequence identity with Clostridium species.

We have investigated hydrogen (H2) production by the cellulose-degrading anaerobic bacterium, Clostridium thermocellum. In the following experiments, batch-fermentations were carried out with cellobiose at three different substrate concentrations to observe the effects of carbon-limited or carbon-excess conditions on the carbon flow, H2-production, and synthesis of other fermentation end products, such as ethanol and organic acids. Rates of cell growth were unaffected by different substrate concentrations. H2, carbon dioxide (CO2), acetate, and ethanol were the main products of fermentation. Other significant end products detected were formate and lactate. In cultures where cell growth was severely limited due to low initial substrate concentrations, hydrogen yields of 1 mol H2/mol of glucose were obtained. In the cultures where growth ceased due to carbon depletion, lactate and formate represented a small fraction of the total end products produced, which consisted mainly of H2, CO2, acetate, and ethanol throughout growth. In cultures with high initial substrate concentrations, cellobiose consumption was incomplete and cell growth was limited by factors other than carbon availability. H2-production continued even in stationary phase and H2/CO2 ratios were consistently greater than 1 with a maximum of 1.2 at the stationary phase. A maximum specific H2 production rate of 14.6 mmol g dry cell(-1) h(-1) was observed. As cells entered stationary phase, extracellular pyruvate production was observed in high substrate concentration cultures and lactate became a major end product.

The objective of this research was to understand how carbon loading influences hydrogen (H(2)) synthesis and metabolic flow patterns in the thermophilic, cellulolytic bacterium, Clostridium thermocellum. C. thermocellum was cultivated in batch cultures with high (5 g L(-1)) and low (1 g L(-1)) initial concentrations of alpha-cellulose at 60 degrees C. The growth rate of C. thermocellum was 22% lower (0.15 h(-1)) in cultures with low-cellulose concentration compared with cultures with high-cellulose concentrations. Although substrate depletion coincided with the end of log-growth in low-cellulose cultures, the prime reason for growth arrest in high-cellulose cultures was not identified. Ethanol, acetate, and formate were the major soluble end-products with concomitant release of H(2) and CO(2) under both conditions. Lactate appeared during the late log phase in high-carbon cultures when pH dropped below 6.4 and became the major end-product in stationary phase. During the exponential phase of cell growth, significantly higher yields for H(2) and acetate (1.90 +/- 0.14 and 1.11 +/- 0.04 mol/mol glucose equivalent, respectively) were obtained from low-cellulose cultures compared to those from high-cellulose cultures. The maximum specific rate of H(2) production, 6.41 +/- 0.13 mmol H(2)/g dry cell/h, obtained during the exponential phase from low-carbon cultures was about 37% higher than that obtained from high-carbon cultures.

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Combinatorial effects of influential growth nutrients were investigated in order to enhance hydrogen (H2) production during direct conversion of cellulose by Clostridium thermocellum DSM 1237. A central composite face-centered design and response surface methodology (RSM) were applied to optimize concentrations of cellulose, yeast extract (YE), and magnesium chloride (Mg) in culture. The overall optimum composition generated by the desirability function resulted in 57.28 mmol H2/L-culture with 1.30 mol H2/mol glucose and 7.48 mmol/(g·cell·h) when cultures contained 25 g/L cellulose, 2 g/L YE, and 1.75 g/L Mg. Compared with the unaltered medium, the optimized medium produced approximately 3.2-fold more H2 within the same time-frame with 50% higher specific productivity, which are also better than previously reported values from similar studies. Nutrient composition that diverted carbon and electron flux away from H2 promoting ethanol production was also determined. This study represents the first investigation dealing with multifactor optimization with RSM for H2 production during direct cellulose fermentation.